EP2308954B1 - Procédé de production d'un phospholipide à pureté élevée et d'une sphingomyéline à pureté élevée et glycérophospholipide du type plasmalogène obtenu au moyen dudit procédé - Google Patents

Procédé de production d'un phospholipide à pureté élevée et d'une sphingomyéline à pureté élevée et glycérophospholipide du type plasmalogène obtenu au moyen dudit procédé Download PDF

Info

Publication number
EP2308954B1
EP2308954B1 EP09766757A EP09766757A EP2308954B1 EP 2308954 B1 EP2308954 B1 EP 2308954B1 EP 09766757 A EP09766757 A EP 09766757A EP 09766757 A EP09766757 A EP 09766757A EP 2308954 B1 EP2308954 B1 EP 2308954B1
Authority
EP
European Patent Office
Prior art keywords
purity
crude
sphingomyelin
plpe
glycerophospholipid
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
EP09766757A
Other languages
German (de)
English (en)
Other versions
EP2308954A4 (fr
EP2308954A1 (fr
Inventor
Yoshitaka Nadachi
Siro Mawatarl
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Marudai Food Co Ltd
Boocs Medical Corp
Umeda Jimusho Ltd
Original Assignee
Marudai Food Co Ltd
Boocs Medical Corp
Umeda Jimusho Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Marudai Food Co Ltd, Boocs Medical Corp, Umeda Jimusho Ltd filed Critical Marudai Food Co Ltd
Publication of EP2308954A1 publication Critical patent/EP2308954A1/fr
Publication of EP2308954A4 publication Critical patent/EP2308954A4/fr
Application granted granted Critical
Publication of EP2308954B1 publication Critical patent/EP2308954B1/fr
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B1/00Production of fats or fatty oils from raw materials
    • C11B1/10Production of fats or fatty oils from raw materials by extracting
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23JPROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
    • A23J7/00Phosphatide compositions for foodstuffs, e.g. lecithin
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L33/00Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • A23L33/10Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
    • A23L33/115Fatty acids or derivatives thereof; Fats or oils
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B11/00Recovery or refining of other fatty substances, e.g. lanolin or waxes
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B13/00Recovery of fats, fatty oils or fatty acids from waste materials
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/74Recovery of fats, fatty oils, fatty acids or other fatty substances, e.g. lanolin or waxes

Definitions

  • the present invention relates to a process for producing a high-purity sphingomyelin, in particular, a human sphingomyelin, and a high-purity plasmalogen-form glycerophospholipid, which are useful as materials of functional foods, medicinal products, cosmetics etc., from a biological material, preferably from poultry, by simple procedures at high yields.
  • Lipids refer to substances that have a long-chain fatty acid or similar hydrocarbon chain in a molecule, and that are present in an organ or derived from a zoic organ. Lipids can be classified into simple lipids and complex lipids. Simple lipids are composed of C, H and O, and are generally soluble in acetone; the simple lipid triacylglycerol is present as an energy reservoir in a fat tissue of an animal body. On the other hand, complex lipids are a group of lipids containing P of phosphoric acid, N of a base etc. Therefore, complex lipids are composed of a hydrophobic part (fatty acid part) and a hydrophilic part (phosphoric acid and base parts), and exhibit an amphophilic nature. Generally, the above simple lipids are soluble in acetone, while the complex lipids are insoluble in acetone. Such complex lipids are a constituent of biomembranes.
  • the above complex lipids can be classified into (1) glycerophospholipids (such as phosphatidylcholine (also known as lecithin), phosphatidylethanolamine, etc.), (2) sphingophospholipids (such as sphingomyelin, ceramide ciliatine, etc.), (3) sphingoglycolipids (such as cerebroside, sulfatide, ganglioside, etc.) and (4) glyceroglycolipids (such as lipids in which various saccharides bond to diacyl glycerol existing in microorganisms or higher plants).
  • the above (2) sphingophospholipids and (3) sphingoglycolipids are generically referred to as "sphingolipids".
  • the above glycerophospholipid is a generic term for lipids having glycerophosphoric acid backbone in their structure, and includes phosphatidylcholine (lecithin), phosphatidylethanolamine, diphosphatidylglycerol, etc.
  • Many lipids belonging to this glycerophospholipid are those in which the non-polar portion is a fatty acid ester, while some are of a plasmalogen form having a vinyl ether bond.
  • the above glycerophospholid is important as a constituent of biomembranes; above all, the plasmalogen-form glycerophospholipid has high radical sensitivity due to its vinyl-ether bond, and, hence, in recent years has been highlighted as a phospholipid having anti-oxidation nature. It has recently been reported that the plasmalogen-form glycerophospholipid contributes to oxidation-stability of phospholipid membrane containing cholesterol through a mechanism different from ⁇ -tocopherol (vitamin E) that is an anti-oxidation constituent of cell membrane (for example, see Non-patent Literature 1).
  • vitamin E ⁇ -tocopherol
  • Non-patent Literature 2 the plasmalogen-form glycerophospholipid not only takes part in the oxidation resistance of cell membrane and lipoprotein, but also has an important role in the information communication system of cells (for example, see Non-patent Literature 2).
  • the above plasmalogen-form glycerophospholipid is expected to have the function of preventing the death of brain nerve cells in dementia. Under the circumstances, however, no supply source that is safe and makes a large amount available has been found.
  • sphingolipid is a generic term for lipids having a long-chain base such as sphingosine, and it is composed mainly of sphingoglycolipid and sphlngophospholipid as described above.
  • the sphingoglycolipid contains a long-chain base such as sphingosine, phytosphingosine etc. in addition to saccharide and long-chain fatty acid.
  • sphingoglycolipid The simplest sphingoglycolipid is cerebroside; apart from cerebroside, sphingoglycolipid includes sulfatide in which a sulfuric acid group is bonded thereto, ceramide oligohexoside in which several molecules of neutral saccharide are bonded thereto, ganglioside in which sialic acid is bonded thereto, etc. These lipids are present in the cell cortex, and are thought to take part in a recognitive mechanism.
  • Sphingophospholipids are classified into derivatives of ceramide 1-phosphoric acid and derivatives of ceramide 1-phosphonic acid.
  • Sphingomyelin is a well-known example of the former, while ceramide ciliatine (ceramide aminoethylphosphonic acid) is a well-known example of the latter.
  • sphingolipids are highlighted since it has been shown in recent years that ceramide, sphingosine, sphingosine-1-phosphoric acid, etc., which are decomposition metabolites thereof, take part in the information communication in cells. Further, sphingolipids take part in the formation of a membrane microdomain called a "raft" together with cholesterol, etc., and it has been shown that this microdomain plays an important role as a site of information communication; accordingly, further increased attention has been paid to sphingolipids.
  • sphingolipids have hitherto been extracted from cow brains and utilized; however, those that are derived from cereals or fungi are now used from a safety standpoint. Since, however, sphingoid bases constituting sphingolipids derived from cereals or fungi differ from those of mammals, there is a problem that their utility in organisms is low compared with human-form sphingolipids.
  • sphingomyelin when a relatively large amount of sphingomyelin is produced from total lipids of foods or animal tissues, it is produced by eluting it stepwise by means of column chromatography using silicic acid, etc., or by fractionating it stepwise according to a solvent fractionation method. Both of these require complicated procedures.
  • solvent fractionation method it is a general practice to employ a method in which acetone is added to total lipids to precipitate complex lipid (phospholipid) (insoluble portion), after which the insoluble portion is washed with ether to remove glycerophospholipid, and the residue is taken as a crude sphingolipid fraction.
  • This fraction contains not only sphingomyelin, but also glycerosphingolipids such as cerebroside.
  • the phospholipid of chicken skin contains a great deal of human-form sphingomyelin and plasmalogen-form glycerophospholipid.
  • J. Am. Oil Chem. Soc., vol. 85, 2008, pages 427 to 433 discloses a concentration method of complex lipids from the skin of mature laying hens. Therein, the complex lipids are separated from an ethanol extract of minced skin by solvent fractionation with a hexane/ethanol system.
  • an object of the present invention is to provide a process for producing high-purity sphingomyelin, in particular, a human sphingomyelin, and high-purity plasmalogen-form glycerophospholipid from a biological material by simple procedures at high yields.
  • the present inventors conducted intensive studies to achieve the foregoing object, and found that the above object can be achieved by processing a biological material in a specific manner. Based on this finding, the inventors completed the present invention.
  • this invention provides:
  • the present invention provides a process for producing high-purity sphingomyelin, in particular, human sphingomyelin, and high-purity plasmalogen-form glycerophospholipid, which are useful as materials of functional foods, medicinal products, cosmetics etc., from a biological material, preferably from poultry, by simple procedures at high yields; generally a high-purity sphingomyelin and a high-purity plasmalogen-form glycerophospholipid is obtained by the process.
  • the process for producing high-purity phospholipid according to the present invention comprises Step (A), Step (B), Step (C), Step (D) and Step (E).
  • This Step (A) is a step in which the dried total lipids extracted from a biological material are subjected to extraction treatment with a mixture solution of an aliphatic hydrocarbon solvent and a water-soluble ketone solvent to separate an insoluble portion composed mainly of sphingomyelin and a soluble portion.
  • the biological material used as a raw material in Step (A) is not particularly limited, and various biological materials may be used as long as they contain a sphingomyelin, in particular, a human sphingomyelin, and a plasmalogen-form glycerophospholipid.
  • various biological materials poultry is preferable in terms of its availability, content of target substance, and economical efficiency; further, culled laying hens and culled breeding hens of broilers (male/female) are more preferable. Examples of regions include bowel, neck, wing, leg, head, bone, etc., as well as epidermis and breast.
  • the aforementioned culled laying hens refer to laying hens subjected to culling. Culling is performed, for example, by fasting white strain laying hens (Julia) or brown strain laying hens (Boris Brown, Sonia) for several days at an average age of 550 days old.
  • those subjected to forced molting are particularly preferred for the following reasons.
  • Forced molting is performed by fasting laying hens of about 500 and several days old, which have decreased laying efficiency, for 10 to 14 days, and then compulsorily de-feathering the hens. This process reproduces the functions of the laying hen, thereby prolonging the laying period by about another 200 days. These forced-molted laying hens are culled in the same way as above.
  • these forced-molted laying hens are subjected to another forced molting at about 700 days old, thereby further extending the laying period by up to 900 days (this period is referred to as double forced molting).
  • An appropriate time of culling of the laying hens is at 500 to 950 days old, more preferably 550 to 900 days old, further preferably 600 to 750 days old.
  • the laying hens in particular, those of 500 days old or older, are under greater stress than the other hens. Therefore, as evident from the described function reproduction shown by the increase in laying efficiency, the secretions of various function-expressing components, such as minor components including hormones, vitamins and cytokines, whose contents are decreased in aged hens, increase, thereby preventing the decrease of the contents by aging.
  • various function-expressing components such as minor components including hormones, vitamins and cytokines, whose contents are decreased in aged hens, increase, thereby preventing the decrease of the contents by aging.
  • broiler breeding hens male/female Chunky and Cobb
  • Broilers are generally raised in good condition; robustness is most important in raising male broilers, while good health is most important for female broilers, as they are required to efficiently produce healthy fertilized ovum.
  • An appropriate time for the culling of broilers is at 300 to 550 days old, more preferably 370 to 550 days old, further preferably 400 to 450 days old.
  • Step (A) total lipids are extracted from a biological material, for example, from epidermis or breast meat of a culled laying hen or culled breeding hen. The extracted total lipids are then dried.
  • chicken skin When using chicken skin, it is preferable to use minced or powdered chicken skin.
  • chicken skin may be defatted to remove the fat content to some extent before being minced or powdered.
  • defatting treatment of chicken skin there may be employed a mechanical method, a method of immersion in hot water under heat, a direct heating method, a method using an aliphatic hydrocarbon solvent (n-hexane), or the like.
  • breast meat it is preferable to use minced breast meat.
  • total lipids are extracted from the thus-obtained minced or powdered chicken skin or minced chicken breast meat using a solvent, and are dried to obtain dried total lipids.
  • a solvent various solvents may be used; however, it is preferable to use a mixture solution of n-hexane and isopropanol.
  • the mixture solution preferably contains n-hexane and isopropanol at a capacity ratio of 8:2 to 4:6, more preferably 7:3 to 5:5.
  • the extraction may be performed by a usual method.
  • the solvent is distilled off from the resulting extract by a conventional method using a rotary evaporator or the like, or by introducing nitrogen gas, thereby obtaining dried total lipids.
  • the dried total lipids obtained in the above manner are subjected to extraction treatment with a mixture solution of an aliphatic hydrocarbon solvent and a water-soluble ketone solvent to separate an insoluble portion composed mainly of sphingomyelin (it is also referred to as a "crude sphingomyelin” hereinafter) and a soluble portion.
  • Examples of the aliphatic hydrocarbon solvent as one component in the mixture solution that is used for the extraction treatment of the dried total lipids in Step (A) include n-pentane, isopentane, n-hexane, isohexane, n-heptane, isoheptane, cyclopentane and/or cyclohexane. They may be used singly, or in a combination of two or more. Among them, n-hexane is suitable.
  • water-soluble ketone solvent examples include acetone and methyl ethyl ketone. Among them, acetone is suitable.
  • the capacity ratio thereof is preferably 4:6 to 6:4, more preferably 4.5:5.5 to 5.5:4.5.
  • the amount of the mixture solution for use is normally approximately 10 to 30 ml per gram of the dried total lipids.
  • the amount of the mixture solution is less than 10 mL, the extraction treatment cannot be sufficiently carried out, and the purity and yield of sphingomyelin in the insoluble portion may decrease.
  • the amount of the mixture solution for use is preferably 15 to 25 mL per gram of the dried total lipids.
  • the extraction treatment can be carried out according to a usual method.
  • the liquid obtained after extraction treatment can be separated by centrifugal treatment into a soluble portion and an insoluble portion composed mainly of sphingomyelin.
  • Step (B) the insoluble portion composed mainly of sphingomyelin obtained in Step (A) is washed with a mixture solution of an aliphatic hydrocarbon solvent and a water-soluble ketone solvent, thereby obtaining crude sphingomyelin.
  • Step (B) The aliphatic hydrocarbon solvent and the water-soluble ketone solvent used as components of a mixture solution for the washing process in Step (B) are the same as those described in Step (A).
  • the capacity ratio thereof is preferably 4:6 to 6:4, more preferably 4.5:5.5 to 5.5:4.5.
  • Step (C) is a step in which the insoluble portion obtained in the above Step (A) is subjected to solvent-removing treatment, followed by washing with a water-soluble ketone solvent, thereby obtaining a crude plasmalogen-form glycerophospholipid.
  • Examples of the water-soluble ketone solvent used in Step (C) include acetone and/or methyl ethyl ketone. Among them, acetone is suitable.
  • Step (C) the solvent in the soluble portion obtained in Step (A) is first distilled off, and the residue is washed with a water-soluble ketone solvent, thereby obtaining a crude plasmalogen-form glycerophospholipid.
  • Step (D) is a step in which a glycerophospholipid hydrolase phospholipase is caused to act on the crude sphingomyelin obtained in Step (B) so as to hydrolyze the glycerophospholipid group contained therein, followed by solvent partition to obtain a sphingomyelin having a purity of 90% or more.
  • Step (D) an enzyme phospholipase is caused to act on the crude sphingomyelin obtained in Step (B), so as to hydrolyze the glycerophospholipid group contained therein.
  • the amount of enzyme phospholipase is generally about 0.15 to 0.45 g, preferably about 0.2 to 0.3 g, per gram of the crude sphingomyelin.
  • the reaction temperature is generally about 30 to 70°C, preferably 45 to 55°C.
  • the pH value is generally about 3.5 to 5.5, preferably 4 to 5. For the reaction time, 1 to 5 hours of reaction should be sufficient.
  • sphingomyelin is separated by solvent partition.
  • a preferable example of the solvent used in the solvent partition is a combination of an aliphatic hydrocarbon solvent and a water-soluble ketone solvent.
  • n-hexane is suitable for the aliphatic hydrocarbon solvent
  • acetone is suitable for the water-soluble ketone solvent.
  • the proportion thereof is generally preferably 4:6 to 6:4, more preferably 4.5:5.5 to 5.5:4.5 in capacity ratio.
  • Step (E) is a step in which a glycerophospholipid hydrolase phospholipase is caused to act on the crude sphingomyelin obtained in Step (C) so as to hydrolyze other glycerophospholipid group contained therein, followed by solvent partition to obtain a plasmalogen-form glycerophospholipid having a purity of 40% or more.
  • Step (E) an enzyme phospholipase is caused to act on the crude plasmalogen-form glycerophospholipid obtained in Step (C), so as to hydrolyze other glycerophospholipid group contained in the crude plasmalogen-form glycerophospholipid.
  • the amount of enzyme phospholipase is generally about 0.15 to 0.45 g, preferably about 0.2 to 0.3 g, per gram of the crude plasmalogen-form glycerophospholipid.
  • the reaction temperature is generally about 30 to 70°C, preferably 45 to 55°C.
  • the pH value is generally about 3.5 to 5.5, preferably 4 to 5. For the reaction time, 1 to 5 hours of reaction should be sufficient.
  • solvent partition is performed to extract plasmalogen-form glycerophospholipid.
  • a preferable example of the solvent used in the solvent partition process is a combination of an aliphatic hydrocarbon solvent and a lower alcohol solvent.
  • n-hexane is suitable for the aliphatic hydrocarbon solvent
  • isopropanol is suitable for the lower alcohol solvent.
  • the proportion thereof is generally 8:2 to 4:6, preferably 7:3 to 5.5 in capacity ratio.
  • the aliphatic hydrocarbon solvent layer is washed with water, and the solids content resulting from distillation of the solvent is washed with a mixture solution of an aliphatic hydrocarbon solvent and a water-soluble ketone solvent, preferably a mixture solution of n-hexane and acetone having a capacity ratio of 4:6 to 6:4, followed by centrifugation or the like to separate the solid and the liquid, thereby obtaining high-purity plasmalogen-form glycerophospholipid having a purity of 40% or more, preferably 95% or more, more preferably 99% or more.
  • high-purity plasmalogen-form phosphatidylcholine having a purity of 95% or more, preferably 99.5% or more
  • high-purity plasmalogen-form phosphatidylethanolamine having a purity of 95% or more, preferably 99.5% or more
  • the process of the present invention enables, when using chicken skin as a raw material, production of about 0.2 to 0.6 mass% of a high-purity sphingomyelin generally having a purity of 90% or more, and 0.3 to 2 mass% of high-purity mixed plasmalogen-form glycerophospholipid having a purity of 40% or more, from concentrated deoiled chicken skin.
  • the process also enables, when using chicken breast meat as a raw material, production of about 0.2 to 1 mass% of high-purity mixed plasmalogen-form glycerophospholipid having a purity of 40% or more, and 0.01 to 0.1 mass% of a high-purity sphingomyelin having a purity of 90% or more.
  • Sphingomyelin includes a phosphoric diester bond formed by a primary-alcoholic hydroxyl group of ceramide and choline phosphoric acid, and has a structure of the following formula (I),
  • R-CO represents a fatty-acid residue, and is normally widely present not only in brain tissues, but also in organ tissues of animal bodies.
  • this sphingomyelin is a human-form sphingomyelin having high bioavailability.
  • sphingomyelin as ceramide, sphingosin, sphingosin-1-phosphoric acid, etc., which are metabolites produced by decomposition thereof, participates in information communication in lipids; it has also been revealed that sphingomyelin participates in the formation of a membrane microdomain called a "raft" together with cholesterol etc., and that the microdomain performs an important role as an information communication site. Further, sphingomyelin is expected to have a skin moisture-retaining effect, an effect of preventing a large intestine cancer, and the like.
  • the high-purity plasmalogen-form glycerophospholipid obtained by the process of the present invention mainly contains phosphatidylethanolamine (PE), and partially contains phosphatidylcholine (PC). Approximately 80 mass% of the above PE is plasmalogen-form, and PC contains approximately 30 mass% of a plasmalogen-form.
  • PE phosphatidylethanolamine
  • PC phosphatidylcholine
  • a general glycerophospholipid (lecithin) has an ester bond with an aliphatic acyl group in sn-1 (1 position) of glycerol as shown in the formula (II), while a plasmalogen-form has a vinyl ether bond having an alkenyl group in sn-1 of glycerol as shown in the formula (III).
  • X is an aminoethyl group, it is a phosphatidylethanolamine; and when X is a trimethyl aminoethyl group, it is phosphatidylcholine.
  • the present invention causes an enzyme phospholipase to act on the crude plasmalogen-form glycerophospholipid so as to hydrolyze a general glycerophospholipid group mainly represented by the formula (II), thereby producing a high-purity sphingomyelin having a purity of 90% or more, and a high-purity plasmalogen-form glycerophospholipid having a purity of 40% or more.
  • the above plasmalogen-form glycerophospholipid attracts attention as an oxidation-resisting phospholipid because its vinyl ether bond has high radical sensitivity, and it is known to contribute to the oxidation stability of a phospholipid membrane containing cholesterol. Further, it has been stated that the plasmalogen-form glycerophospholipid not only takes part in the oxidation resistance of cell membrane and lipoprotein, but also plays an important role in the information communication system of cells.
  • the above plasmalogen-form glycerophospholipid is expected to work to prevent the neurocyte death of a brain in dementia, or have an effect on the prevention of the onset of atherosclerosis.
  • the present invention also provides a high-purity sphingomyelin having a purity of 90% or more, and a high-purity plasmalogen-form glycerophospholipid having a purity of 40% or more, which are obtained by the above-described process of the present invention.
  • SM sphingomyelin
  • plPC sphingomyelin
  • plasmalogen-form phosphatidylcholine plasmalogen-form phosphatidylethanolamine, respectively.
  • Frozen minced chicken skin obtained from the green skin of a culled laying hen (Julia, 550 days old) was concentrated by deoiling, followed by a usual freeze-drying process. The freeze-dried mince was subjected to total lipids extraction as shown in FIG. 1-1 . The total lipids were obtained at a yield of 26.8%.
  • Table 1 shows time zone and liquid composition of mobile phases A and B.
  • TEA Triethylamine
  • Example 1 In a comparison between Example 1 and Example 7 with respect to SM and plPE derived from culled laying hen skin, in Example 1 using a general culled laying hen, the yield and purity of the purified plPE were 50% and 95%, respectively, while the yield and purity of the purified SM were 75% and 96.2%, respectively. In contrast, in Example 7 using a culled laying hen subjected to forced molting, the yield and purity of the purified plPE were 55% and 96.2%, respectively, while the yield and purity of the purified SM were 78% and 96.9%, respectively.
  • Example 2 in a comparison between Example 2 and Example 8 with respect to [plPC+plPE] derived from breast meat of culled laying hen, in Example 2 using a general culled laying hen, the total yield and each purity of the purified [plPC+plPE] were 95.4% and 100%, respectively. In contrast, in Example 8 using a culled laying hen subjected to forced molting, the total yield and each purity of the purified [plPC+plPE] were 96.0% and 100%, respectively.
  • the culled laying hen subjected to forced molting had higher yields and purities for both the purified plPE and SM, and higher total yield of the purified [plPC+plPE] than that of a general culled laying hen.
  • the process for producing high-purity phospholipid of the present invention enables production of high-purity sphingomyelin, in particular, a human sphingomyelin, and high-purity plasmalogen-form glycerophospholipid, which are useful as materials of functional foods, medicinal products, cosmetics etc., from a biological material, such as poultry, by simple procedures at high yields.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Biochemistry (AREA)
  • Mycology (AREA)
  • Health & Medical Sciences (AREA)
  • Nutrition Science (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Fats And Perfumes (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)

Claims (6)

  1. Procédé de production d'un phospholipide de pureté élevée, comprenant les étapes suivantes :
    (A) la soumission de lipides totaux séchés extraits d'un matériau biologique à un traitement d'extraction avec une solution d'un mélange d'un solvant d'hydrocarbure aliphatique et d'un solvant de cétone hydrosoluble pour séparer une partie insoluble composée principalement de sphingomyéline et une partie soluble ;
    (B) la soumission de la partie insoluble composée principalement de sphingomyéline, obtenue dans ladite étape (A), à un traitement de lavage avec une solution d'un mélange d'un solvant d'hydrocarbure aliphatique et d'un solvant de cétone hydrosoluble pour obtenir de la sphingomyéline brute ;
    (C) la soumission de la partie soluble, obtenue dans ladite étape (A), à un traitement d'élimination du solvant et ensuite à un traitement de lavage avec un solvant de cétone hydrosoluble pour obtenir un glycérophospholipide du type plasmalogène brut ;
    (D) la provocation d'une phospholipase, qui est la glycérophospholipide hydrolase, à agir sur la sphingomyéline brute, obtenue dans ladite étape (B), pour hydrolyser un groupe glycérophospholipide contenu dans la sphingomyéline brute, et la réalisation d'un partage dans des solvants pour obtenir de la sphingomyéline présentant une pureté de 90 % ou plus ; et
    (E) la provocation d'une phospholipase, qui est la glycérophospholipide hydrolase, à agir sur le glycérophospholipide du type plasmalogène brut obtenu dans ladite étape (C), pour hydrolyser d'autres groupes glycérophospholipides contenus dans le glycérophospholipide du type plasmalogène brut, et la réalisation d'un partage dans des solvants pour obtenir le glycérophospholipide du type plasmalogène présentant une pureté de 40 % ou plus.
  2. Procédé selon la revendication 1, dans lequel le matériau biologique est une volaille.
  3. Procédé selon la revendication 2, dans lequel la volaille est une poule pondeuse réformée et/ou une poule d'élevage réformée.
  4. Procédé selon la revendication 3, dans lequel la poule pondeuse réformée est obtenue à partir d'une poule pondeuse plumée de force.
  5. Procédé selon l'une quelconque des revendications 1 à 4, dans lequel le solvant d'hydrocarbure aliphatique est le n-hexane.
  6. Procédé selon l'une quelconque des revendications 1 à 5, dans lequel le solvant de cétone hydrosoluble est l'acétone.
EP09766757A 2008-06-20 2009-06-19 Procédé de production d'un phospholipide à pureté élevée et d'une sphingomyéline à pureté élevée et glycérophospholipide du type plasmalogène obtenu au moyen dudit procédé Active EP2308954B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2008162119 2008-06-20
PCT/JP2009/061666 WO2009154309A1 (fr) 2008-06-20 2009-06-19 Procédé de production d'un phospholipide à pureté élevée et d'une sphingomyéline à pureté élevée et glycérophospholipide du type plasmalogène obtenu au moyen dudit procédé

Publications (3)

Publication Number Publication Date
EP2308954A1 EP2308954A1 (fr) 2011-04-13
EP2308954A4 EP2308954A4 (fr) 2011-09-21
EP2308954B1 true EP2308954B1 (fr) 2012-10-24

Family

ID=41434216

Family Applications (1)

Application Number Title Priority Date Filing Date
EP09766757A Active EP2308954B1 (fr) 2008-06-20 2009-06-19 Procédé de production d'un phospholipide à pureté élevée et d'une sphingomyéline à pureté élevée et glycérophospholipide du type plasmalogène obtenu au moyen dudit procédé

Country Status (5)

Country Link
US (1) US8524282B2 (fr)
EP (1) EP2308954B1 (fr)
JP (1) JP5430566B2 (fr)
CN (1) CN102099453B (fr)
WO (1) WO2009154309A1 (fr)

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011083827A1 (fr) * 2010-01-06 2011-07-14 株式会社レオロジー機能食品研究所 Agent de néogénèse de cellules nerveuses cérébrales
JP5847086B2 (ja) * 2010-09-24 2016-01-20 株式会社藤野ブレインリサーチ 抗中枢神経系炎症剤
FR3000959B1 (fr) 2013-01-14 2015-08-21 Holis Technologies Nouveaux intermediaires de synthese permettant d'acceder avec de bons rendements a des derives de sphingosines, ceramides et sphingomyelines
JP6349532B2 (ja) 2014-12-08 2018-07-04 志郎 馬渡 エーテルリン脂質およびその製造方法
EP3309242A4 (fr) * 2015-05-12 2018-12-26 Takehiko Fujino Procédé de production d'étherphospholipides
CN105732701A (zh) * 2016-01-28 2016-07-06 马腾 一种从生物材料制造以缩醛磷脂为有效成分的治疗脑神经疾病的物质的生产方法
KR20190003570A (ko) * 2016-05-02 2019-01-09 우메다 지무쇼 리미티드 안전한·안정된 플라스마로겐과 그 제제 및 인지증의 미병 상태의 판정 방법
WO2017191838A1 (fr) * 2016-05-02 2017-11-09 有限会社梅田事務所 Plasmalogène sûr et stable, sa formulation et procédé permettant d'évaluer un état pré-symptomatique de démence
JP6603923B2 (ja) * 2016-05-02 2019-11-13 有限会社梅田事務所 認知機能の改善作用を有する鶏胸肉由来プラズマローゲン組成物及びこれを含有して成る認知機能の向上及び/又は改善用食品組成物又はサプリメント
US10653708B2 (en) 2017-06-16 2020-05-19 Institute of Rheological Functions of Food Uses of ether phospholipids in treating diseases
JP6542408B1 (ja) * 2018-02-21 2019-07-10 丸大食品株式会社 リン脂質濃縮物生産方法
CN109369705B (zh) * 2018-10-12 2020-10-30 浙江工商大学 利用钛基介孔硅胶复合材料提取三角帆蚌缩醛磷脂的方法
CN114644650A (zh) * 2020-12-21 2022-06-21 广州白云山汉方现代药业有限公司 一种从蛋黄粉中提取高纯度鞘磷脂的方法

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0439398A (ja) * 1990-06-05 1992-02-10 Snow Brand Milk Prod Co Ltd 動物性油脂の親水性有機溶媒抽出物から脂質画分を分画精製する方法
JP3439498B2 (ja) 1993-02-05 2003-08-25 太陽化学株式会社 スフィンゴミエリンの精製方法
KR100225669B1 (ko) * 1997-04-18 1999-10-15 유병택 효소를 이용한 고순도 인지질의 생산방법
JP2006151818A (ja) 2004-11-25 2006-06-15 Shu Uemura:Kk 皮膚化粧料
US20080151369A1 (en) * 2005-05-07 2008-06-26 Welch Stephen R Lenticular display with a three dimensional optical mat
EP1960534A4 (fr) 2005-12-15 2009-03-25 Univ New York State Res Found Methodes enzymatiques permettant de mesurer la sphingomyeline et la phosphatidylcholine dans le plasma et le tissu
JP5185539B2 (ja) 2007-01-26 2013-04-17 有限会社梅田事務所 スフィンゴミエリンおよびプラズマローゲン型グリセロリン脂質の製造方法
JP5774816B2 (ja) * 2007-05-28 2015-09-09 有限会社梅田事務所 リン脂質含有機能性素材の製造方法およびプラズマローゲン型グリセロリン脂質の製造方法

Also Published As

Publication number Publication date
US8524282B2 (en) 2013-09-03
CN102099453B (zh) 2013-09-25
EP2308954A4 (fr) 2011-09-21
JPWO2009154309A1 (ja) 2011-12-01
US20110160471A1 (en) 2011-06-30
CN102099453A (zh) 2011-06-15
EP2308954A1 (fr) 2011-04-13
WO2009154309A1 (fr) 2009-12-23
JP5430566B2 (ja) 2014-03-05

Similar Documents

Publication Publication Date Title
EP2308954B1 (fr) Procédé de production d'un phospholipide à pureté élevée et d'une sphingomyéline à pureté élevée et glycérophospholipide du type plasmalogène obtenu au moyen dudit procédé
KR102704572B1 (ko) 리소포스파티딜콜린 조성물
JP5185539B2 (ja) スフィンゴミエリンおよびプラズマローゲン型グリセロリン脂質の製造方法
JP6349532B2 (ja) エーテルリン脂質およびその製造方法
Schneider Phospholipids
JP6626099B2 (ja) エーテルリン脂質の製造方法
JPH1084880A (ja) 脂質代謝促進作用を有するリン脂質含有組成物
JP3992425B2 (ja) スフィンゴ糖脂質含有物の製造方法
JP7021953B2 (ja) エーテル型グリセロリン脂質の製造方法
JP4359204B2 (ja) 皮膚保湿用食品
JP2717510B2 (ja) 苦味低減化剤の製造法
JP6842093B2 (ja) 学習記憶能力増強剤
JPH1084879A (ja) 肝臓中性脂肪合成抑制作用を有する粗大豆レシチン分画物
JP5610813B2 (ja) 経口摂取用皮膚賦活剤
JP2010159383A (ja) 複合脂質の分離法

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20110118

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO SE SI SK TR

AX Request for extension of the european patent

Extension state: AL BA RS

RIC1 Information provided on ipc code assigned before grant

Ipc: A23L 1/30 20060101ALI20110811BHEP

Ipc: C11B 11/00 20060101AFI20110811BHEP

Ipc: A23J 7/00 20060101ALI20110811BHEP

Ipc: C11B 3/02 20060101ALI20110811BHEP

Ipc: C11B 3/00 20060101ALI20110811BHEP

Ipc: C11B 1/10 20060101ALI20110811BHEP

A4 Supplementary search report drawn up and despatched

Effective date: 20110819

DAX Request for extension of the european patent (deleted)
RIC1 Information provided on ipc code assigned before grant

Ipc: A23J 7/00 20060101ALI20120417BHEP

Ipc: C11B 11/00 20060101AFI20120417BHEP

Ipc: C11B 13/00 20060101ALI20120417BHEP

Ipc: A23L 1/30 20060101ALI20120417BHEP

Ipc: C11B 3/00 20060101ALI20120417BHEP

Ipc: C11B 1/10 20060101ALI20120417BHEP

Ipc: C11B 3/02 20060101ALI20120417BHEP

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO SE SI SK TR

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

REG Reference to a national code

Ref country code: AT

Ref legal event code: REF

Ref document number: 580983

Country of ref document: AT

Kind code of ref document: T

Effective date: 20121115

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 602009010684

Country of ref document: DE

Effective date: 20121227

REG Reference to a national code

Ref country code: AT

Ref legal event code: MK05

Ref document number: 580983

Country of ref document: AT

Kind code of ref document: T

Effective date: 20121024

REG Reference to a national code

Ref country code: NL

Ref legal event code: VDEP

Effective date: 20121024

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130124

Ref country code: SE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20121024

Ref country code: FI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20121024

Ref country code: NL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20121024

Ref country code: IS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130224

Ref country code: HR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20121024

Ref country code: ES

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130204

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LV

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20121024

Ref country code: PT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130225

Ref country code: SI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20121024

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130125

Ref country code: PL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20121024

Ref country code: BE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20121024

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: AT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20121024

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BG

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130124

Ref country code: SK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20121024

Ref country code: CZ

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20121024

Ref country code: DK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20121024

Ref country code: EE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20121024

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: RO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20121024

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed

Effective date: 20130725

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 602009010684

Country of ref document: DE

Effective date: 20130725

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: CY

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20121024

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MC

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20121024

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

REG Reference to a national code

Ref country code: IE

Ref legal event code: MM4A

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20130630

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20130630

Ref country code: IE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20130619

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20121024

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20121024

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 7

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: TR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20121024

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20121024

Ref country code: HU

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT; INVALID AB INITIO

Effective date: 20090619

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20130619

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 8

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 9

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20240502

Year of fee payment: 16

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20240502

Year of fee payment: 16

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: IT

Payment date: 20240513

Year of fee payment: 16

Ref country code: FR

Payment date: 20240509

Year of fee payment: 16